JPH01289070A - Solid electrolyte fuel cell module - Google Patents

Solid electrolyte fuel cell module

Info

Publication number
JPH01289070A
JPH01289070A JP63118769A JP11876988A JPH01289070A JP H01289070 A JPH01289070 A JP H01289070A JP 63118769 A JP63118769 A JP 63118769A JP 11876988 A JP11876988 A JP 11876988A JP H01289070 A JPH01289070 A JP H01289070A
Authority
JP
Japan
Prior art keywords
air
cells
fuel gas
fuel
cell
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
JP63118769A
Other languages
Japanese (ja)
Inventor
Shozo Kaneko
祥三 金子
Tadashi Gengo
義 玄後
Mitsuo Kamisaka
光男 神坂
Masayasu Sakai
正康 坂井
Yasuhiro Yamauchi
康弘 山内
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Mitsubishi Heavy Industries Ltd
Original Assignee
Mitsubishi Heavy Industries Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Mitsubishi Heavy Industries Ltd filed Critical Mitsubishi Heavy Industries Ltd
Priority to JP63118769A priority Critical patent/JPH01289070A/en
Publication of JPH01289070A publication Critical patent/JPH01289070A/en
Pending legal-status Critical Current

Links

Classifications

    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M8/00Fuel cells; Manufacture thereof
    • H01M8/24Grouping of fuel cells, e.g. stacking of fuel cells
    • H01M8/241Grouping of fuel cells, e.g. stacking of fuel cells with solid or matrix-supported electrolytes
    • H01M8/2425High-temperature cells with solid electrolytes
    • H01M8/243Grouping of unit cells of tubular or cylindrical configuration
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/30Hydrogen technology
    • Y02E60/50Fuel cells

Landscapes

  • Life Sciences & Earth Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Manufacturing & Machinery (AREA)
  • Sustainable Development (AREA)
  • Sustainable Energy (AREA)
  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Electrochemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Fuel Cell (AREA)

Abstract

PURPOSE:To obtain a cell of simple structure and high volumetric efficiency by piling up several cells consisting of a porous ceramic substrate, on the both surface of which air electrode, fuel electrode or the like are laminated, through spacers, and flowing fuel gas and air in the respective enclosed spaces. CONSTITUTION:Fuel electrodes 22, air electrodes 23, electrolyte 24, interconnectors 25, protection films 26 and collector leads 27 are laminated on the both surface of a porous ceramic substrate 21 of 50-90% in porosity to construct cells 11a, 11b. These cells are piled up successively through spacers 12, and in the substrate 21 fuel gas F (or air A) and in the space enclosed with the substrate 21 and the spacer 12 air A (or fuel gas F) are flowed respectively to generate electricity. Thereby these cells can be packed 10-100 times more than cylindrical cells to improve the volumetric efficiency, and because of the plate-like structure every member can be produced in a lump to obtain the module structure of high mass productivity easily.

Description

【発明の詳細な説明】 [産業上の利用分野] 本発明は固体電解質燃料電池モジュールの改良に関する
DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention relates to improvements in solid electrolyte fuel cell modules.

[従来の技術と課題] 周知の如く、固体電解質燃料電池(以下、5OFCと呼
ぶ)としては、例えば第6図に示す如く円筒型の構造の
もの又は第7図に示す如<ノ1ニカム型(モノシリツク
)の構造のものが知られている。
[Prior Art and Problems] As is well known, solid electrolyte fuel cells (hereinafter referred to as 5OFC) have a cylindrical structure as shown in FIG. 6, or a non-unicam type as shown in FIG. (monolithic) structure is known.

第6図の5OFCは、円筒状の多孔質セラミックス基体
1の表面に電池薄膜2を形成したものである。この電池
薄膜2は燃料極(又は空気極)、固体電解質及び空気極
(又は燃料極)を順次薄膜状に積層したものである。こ
の5OFCでは、基体1の内側に燃料ガス(又は空気)
を、外側に空気(又は燃料ガス)を流して発電を行う、
そして電流は図中矢印で示すような流路を流れる。
5OFC shown in FIG. 6 has a cell thin film 2 formed on the surface of a cylindrical porous ceramic substrate 1. This battery thin film 2 is a thin film structure in which a fuel electrode (or air electrode), a solid electrolyte, and an air electrode (or fuel electrode) are sequentially laminated. In this 5OFC, fuel gas (or air) is inside the base 1.
Generate electricity by flowing air (or fuel gas) to the outside,
The current then flows through the flow path as indicated by the arrow in the figure.

第7図図示の5OFCは、上述したような電池薄膜3自
体で例えばハニカム状ブロックを形成スるものである。
The 5OFC shown in FIG. 7 is one in which the battery thin film 3 itself as described above forms, for example, a honeycomb-shaped block.

この5OFCでは、図中Fで示す領域に燃料ガスを、A
で示す領域に空気を夫々流す。そして、電流は図中矢印
で示すような流路を流れる。
In this 5OFC, fuel gas is supplied to the area indicated by F in the figure, and
Air is flowed into the areas indicated by . The current then flows through the flow path as indicated by the arrow in the figure.

しかしながら、円筒型5OFCの場合その構造はシンプ
ルであるが、単位体積′当りの電池有効面積が小さく、
体積効率が低い。
However, although the cylindrical 5OFC has a simple structure, the effective battery area per unit volume is small;
Volumetric efficiency is low.

一方、第7図図示あるいはこれと類似のハニカム型5O
FCの場合、高い体積効率は基体できるものの、電池薄
膜3自体で全体構造を形成するため強度及び組立て上の
問題があり、実際には試作すら完成していない。また、
形態が複雑のため製造することはかなり難しい。特に、
その積層構造のため、大型のものを製作することは焼結
の面で不可能に近い。
On the other hand, a honeycomb type 5O shown in FIG. 7 or similar to this
In the case of FC, although high volumetric efficiency can be achieved as a base, since the entire structure is formed from the battery thin film 3 itself, there are problems in terms of strength and assembly, and in fact, even a prototype has not been completed. Also,
It is quite difficult to manufacture due to its complicated shape. especially,
Because of its laminated structure, it is nearly impossible to manufacture large-sized ones from a sintering perspective.

本発明は上記事情に鑑みてなされたもので、従来の円筒
型の場合のようなシンプルな構造を有し、しかもハニカ
ム型の場合のように体積効率のよい固体電解質燃料電池
モジュールを提供することを目的とする。
The present invention has been made in view of the above circumstances, and it is an object of the present invention to provide a solid electrolyte fuel cell module that has a simple structure like the conventional cylindrical type and has good volumetric efficiency like the honeycomb type. With the goal.

[課題を解決するための手段] 本発明は、ポーラスなセラミックス基板の両面に空気極
、燃料極、電解質及びインタコネクタを積層してセルを
構成し、このセルを燃料ガス又は空気通過用のスペーサ
を介して積重ね、前記基体中又は基体、スペーサで囲ま
れた領域に燃料ガス。
[Means for Solving the Problems] The present invention comprises a cell by laminating an air electrode, a fuel electrode, an electrolyte, and an interconnector on both sides of a porous ceramic substrate, and this cell is connected to a spacer for passage of fuel gas or air. Stack the fuel gas into the substrate or into the substrate, an area surrounded by spacers.

空気を夫々通すことを要旨とする。The gist is to allow air to pass through each.

[作用] 本発明によれば、 ■電池有効面積を円筒型5OFCに比べ同一体積に10
〜100倍に詰めることができ、体積効率を高くするこ
とができる。
[Function] According to the present invention, the effective area of the battery is reduced by 10% in the same volume compared to a cylindrical 5OFC.
It can be packed up to 100 times more, increasing volumetric efficiency.

■板状構造なので、燃料極、空気極、電解質などの各部
材を一括して形成でき、量産性に優れている。
■Since it has a plate-like structure, each component such as the fuel electrode, air electrode, and electrolyte can be formed all at once, making it excellent for mass production.

■板状構造なので、モジュールの構成が容易となる。■Since it has a plate-like structure, it is easy to configure the module.

[実施例] 以下、本発明の一実施例について第1図〜第4図を参照
して説明する。
[Example] Hereinafter, an example of the present invention will be described with reference to FIGS. 1 to 4.

第1図は、本発明の一実施例に係る5OFCモジユール
の概略を示すものである。
FIG. 1 schematically shows a 5OFC module according to an embodiment of the present invention.

図中のlla、llbは、夫々セルである。これらのセ
ルlla、llb間には、複数のスペーサ12が設けら
れている。ここで、スペーサ12はセルの保護膜の上に
位置するように配置され、セルを構成する空気極又は燃
料極が出来るだけ空気又は燃料ガスに触れるようになっ
ている。また、前記セル11a上には、スペーサ12を
介して通路用板13が設けられている。ここで、前記セ
ル11a、llb内には、(実線)矢印で示す如く燃料
ガスF(又は空気A)が通り、セル11a。
lla and llb in the figure are cells, respectively. A plurality of spacers 12 are provided between these cells lla and llb. Here, the spacer 12 is arranged so as to be located on the protective film of the cell, so that the air electrode or fuel electrode constituting the cell comes into contact with air or fuel gas as much as possible. Furthermore, a passage plate 13 is provided on the cell 11a with a spacer 12 interposed therebetween. Here, fuel gas F (or air A) passes through the cells 11a and llb as shown by (solid line) arrows, and the cells 11a and llb pass through.

11b(あるいはセル11a1通路用板13)とスペー
サ12で囲まれた領域には空気A(又は燃料ガスF)が
通るようになっている。なお、(点線)矢印の如く燃料
ガスF、空気Aを通過させてもよい。また、第1図の場
合は燃料ガスFと空気Aが平行に流れる場合であるが、
この他第5図に示すように燃料ガスFと空気Aを交差し
て流してもよいし、あるいは対向するように流してもよ
い。
Air A (or fuel gas F) is allowed to pass through the area surrounded by cell 11b (or cell 11a1 passage plate 13) and spacer 12. Note that fuel gas F and air A may be passed through as shown by the (dotted line) arrow. Also, in the case of Fig. 1, the fuel gas F and air A flow in parallel,
In addition, as shown in FIG. 5, the fuel gas F and the air A may be allowed to flow across each other, or may be allowed to flow oppositely.

前記セルlla、llbは第2図〜第4図に示すように
なっている。図中の21はの燃料ガスFまたは空気Aを
通過させるポーラスなセラミックス基板(フォー、ムセ
ラミックス基板)である。この基板21は、具体的には
例えばアルミナ、CS Z (Calcium S t
ab1]1zcd Z 1reonla )等のセラミ
ックより作られた一定の強度のある厚み500p〜51
1■程度の板で、気孔率は50〜90%程度である。
The cells lla and llb are as shown in FIGS. 2 to 4. Reference numeral 21 in the figure is a porous ceramic substrate through which the fuel gas F or air A passes. Specifically, this substrate 21 is made of, for example, alumina, CS Z (Calcium S t
ab1] 1zcd Z 1reonla) etc. Thickness 500p to 51 with a certain strength
The porosity of the plate is approximately 50 to 90%.

前記基板21の両面には、燃料極22.空気極23、電
解質24.インタコネクタ25、更に保護膜26が適宜
形成されてセルが構成されている。
Fuel electrodes 22. are provided on both sides of the substrate 21. Air electrode 23, electrolyte 24. An interconnector 25 and a protective film 26 are appropriately formed to constitute a cell.

なお、図中の27はリードである。ここで、前記燃料極
22は厚さ100p〜IIImで、Ni系サーメット、
Co系サーメット又は順Ni、Coなどが用いられる。
Note that 27 in the figure is a lead. Here, the fuel electrode 22 has a thickness of 100p to IIIm, and is made of Ni-based cermet,
Co-based cermet or ordered Ni, Co, etc. are used.

前記空気極23は厚さ100p〜1■で、ペロブスカイ
ト系結晶構造の酸化物導電材が用いられる。前記電解質
24の材料としては、Y S Z (Yttrla S
 tabili、zed Z 1rconla ) 。
The air electrode 23 has a thickness of 100p to 1cm, and is made of an oxide conductive material having a perovskite crystal structure. As the material of the electrolyte 24, Y S Z (Yttrla S
tabili, zed Z 1rconla).

系 Ce系、Bi書等が用いられる。前記インタコネクタ2
5.リード27は、還元と同時に酸化にも強い必要があ
り、NI Cr、NI Aノ、NiAノ。
Types such as Ce type, Bi type, etc. are used. The interconnector 2
5. Lead 27 must be resistant to both reduction and oxidation, such as NI Cr, NI A, and NiA.

Fe Ni Coなど耐熱耐酸化合金の他、La Cr
O3等の耐還元性の強いペロブスカイトも用いられる。
In addition to heat-resistant and oxidation-resistant alloys such as Fe Ni Co, La Cr
Perovskites with strong reduction resistance such as O3 are also used.

なお、前記セルでは、円筒型縞セルと同様に板厚に沿っ
た方向に電流を流す縞状構造となりている(第4図参照
)。
Note that the cell has a striped structure in which current flows in the direction along the plate thickness, similar to the cylindrical striped cell (see FIG. 4).

しかして、上記実施例によれば、フオームセラミックス
基板21の両面に燃料極22.空気極23、電解質24
及びインタコネクタ25を適宜積層してセルを構成し、
こうしたセルを複数個スペーサ12を介して積層ね、前
記基体21中に燃料ガス(又は空気)を通し、かつ基体
、スペーサ12(あるいは基体1通路用板13)で囲ま
れた領域に空気(又は燃料ガス)を通す構成となってい
る。従って、 ■電池有効面積を円筒型5OFCに比べ同一体積に10
〜100倍に詰めることができ、体積効率を高くするこ
とができる。
According to the embodiment described above, fuel electrodes 22. Air electrode 23, electrolyte 24
and interconnectors 25 are laminated as appropriate to constitute a cell,
A plurality of such cells are stacked with spacers 12 in between, and fuel gas (or air) is passed through the base 21, and air (or It is configured to allow fuel gas (fuel gas) to pass through. Therefore, ■The effective area of the battery is 10% compared to the cylindrical 5OFC for the same volume.
It can be packed up to 100 times more, increasing volumetric efficiency.

■板状構造なので、燃料極22.空気極23゜電解質2
4などの各部材を一括して形成でき、量産性に優れてい
る。
■Since it has a plate-like structure, the fuel electrode 22. Air electrode 23° Electrolyte 2
Each member such as 4 can be formed at once, and is excellent in mass productivity.

■板状構造なので、モジュールの構成が容易となる。■Since it has a plate-like structure, it is easy to configure the module.

■セル両端で集電が可能なのでモジュール集電が容易で
ある。
■Module current collection is easy because current can be collected at both ends of the cell.

■モジュール内で一部が破損しても、保修が容易である
■Even if a part of the module is damaged, maintenance is easy.

[発明の効果] 以上詳述した如く本発明によれば、従来の円筒型の場合
のようなシンプルな構造を有し、しかもハニカム型の場
合のように体積効率のよい等種々の優れた効果を有する
固体電解質燃料電池モジュールを提供できる。
[Effects of the Invention] As detailed above, according to the present invention, it has a simple structure like the conventional cylindrical type, and has various excellent effects such as good volumetric efficiency like the honeycomb type. A solid electrolyte fuel cell module having the following can be provided.

【図面の簡単な説明】[Brief explanation of the drawing]

第1図は本発明の一実施例に係る5OFCモジユールの
概略を示す斜視図、第2図は同モジュールを構成するセ
ルの断面図、第3図は第2図の平面図、第4図は第2図
のセルにおける電流の流れを示す説明図、第5図は第1
図の5OFCモジユールとは異なるガスの流れを説明す
るための斜視図、第6図及び第7図は夫々従来の5OF
Cの説明図である。 11a、1lb−・・セル、12 ・・・スペーサ、2
1・・・セラミックス基板、22・・・燃料極、・23
・・・空気極、24・・・電解質、25・・・インタコ
ネクタ、26・・・保護膜。 出願人代理人 弁理士 鈴江武彦 第1図 第2図 第3図 第4図 第5図 第6図 3′ 第7図
FIG. 1 is a perspective view schematically showing a 5OFC module according to an embodiment of the present invention, FIG. 2 is a cross-sectional view of cells constituting the module, FIG. 3 is a plan view of FIG. 2, and FIG. An explanatory diagram showing the flow of current in the cell in Fig. 2, and Fig. 5 in the cell in Fig. 1.
A perspective view to explain the gas flow different from that of the 5OFC module shown in the figure, Figures 6 and 7 are respectively the conventional 5OFC module.
FIG. 11a, 1lb-- Cell, 12... Spacer, 2
1... Ceramic substrate, 22... Fuel electrode, 23
... air electrode, 24 ... electrolyte, 25 ... interconnector, 26 ... protective film. Applicant's Representative Patent Attorney Takehiko Suzue Figure 1 Figure 2 Figure 3 Figure 4 Figure 5 Figure 6 Figure 3' Figure 7

Claims (1)

【特許請求の範囲】[Claims] ポーラスなセラミックス基板の両面に空気極、燃料極、
電解質及びインタコネクタを積層してセルを構成し、こ
のセルを燃料ガス又は空気通過用のスペーサを介して積
重ね、前記基体中又は基体、スペーサで囲まれた領域に
燃料ガス、空気を夫々通すことを特徴とする固体電解質
燃料電池モジュール。
Air electrode, fuel electrode,
A cell is formed by stacking an electrolyte and an interconnector, and the cells are stacked with a spacer for passage of fuel gas or air interposed therebetween, and the fuel gas and air are passed through the base body or a region surrounded by the base body and the spacer, respectively. A solid electrolyte fuel cell module featuring:
JP63118769A 1988-05-16 1988-05-16 Solid electrolyte fuel cell module Pending JPH01289070A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP63118769A JPH01289070A (en) 1988-05-16 1988-05-16 Solid electrolyte fuel cell module

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP63118769A JPH01289070A (en) 1988-05-16 1988-05-16 Solid electrolyte fuel cell module

Publications (1)

Publication Number Publication Date
JPH01289070A true JPH01289070A (en) 1989-11-21

Family

ID=14744614

Family Applications (1)

Application Number Title Priority Date Filing Date
JP63118769A Pending JPH01289070A (en) 1988-05-16 1988-05-16 Solid electrolyte fuel cell module

Country Status (1)

Country Link
JP (1) JPH01289070A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2004537143A (en) * 2001-07-24 2004-12-09 ロールス・ロイス・ピーエルシー Solid oxide fuel cell stack

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2004537143A (en) * 2001-07-24 2004-12-09 ロールス・ロイス・ピーエルシー Solid oxide fuel cell stack

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